CN111807817A - Mullite whisker-attapulgite porous ceramic with high specific surface area and preparation method thereof - Google Patents
Mullite whisker-attapulgite porous ceramic with high specific surface area and preparation method thereof Download PDFInfo
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- CN111807817A CN111807817A CN202010716998.0A CN202010716998A CN111807817A CN 111807817 A CN111807817 A CN 111807817A CN 202010716998 A CN202010716998 A CN 202010716998A CN 111807817 A CN111807817 A CN 111807817A
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- attapulgite
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- 239000000919 ceramic Substances 0.000 title claims abstract description 154
- 229960000892 attapulgite Drugs 0.000 title claims abstract description 133
- 229910052625 palygorskite Inorganic materials 0.000 title claims abstract description 133
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 229910052863 mullite Inorganic materials 0.000 title claims abstract description 89
- 238000002360 preparation method Methods 0.000 title claims abstract description 23
- 150000003839 salts Chemical class 0.000 claims abstract description 73
- 238000000034 method Methods 0.000 claims abstract description 60
- 238000002156 mixing Methods 0.000 claims abstract description 40
- 238000000498 ball milling Methods 0.000 claims abstract description 39
- 239000011812 mixed powder Substances 0.000 claims abstract description 29
- 239000000843 powder Substances 0.000 claims abstract description 26
- 230000008569 process Effects 0.000 claims abstract description 25
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims abstract description 22
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims abstract description 17
- 238000009694 cold isostatic pressing Methods 0.000 claims abstract description 17
- 229910004619 Na2MoO4 Inorganic materials 0.000 claims abstract description 16
- 239000011684 sodium molybdate Substances 0.000 claims abstract description 16
- 229910010171 Li2MoO4 Inorganic materials 0.000 claims abstract description 15
- 238000001354 calcination Methods 0.000 claims abstract description 14
- 229910010271 silicon carbide Inorganic materials 0.000 claims abstract description 13
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical group CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 18
- 238000001035 drying Methods 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000009835 boiling Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 9
- 238000007598 dipping method Methods 0.000 claims description 7
- 238000005485 electric heating Methods 0.000 claims description 7
- 238000007605 air drying Methods 0.000 claims description 5
- 238000005470 impregnation Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 28
- 238000005245 sintering Methods 0.000 abstract description 27
- 239000011148 porous material Substances 0.000 abstract description 22
- 239000013078 crystal Substances 0.000 abstract description 18
- 238000011065 in-situ storage Methods 0.000 abstract description 11
- 230000008901 benefit Effects 0.000 abstract description 5
- 238000003825 pressing Methods 0.000 abstract description 2
- 238000001338 self-assembly Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 28
- 239000000126 substance Substances 0.000 description 17
- 230000001276 controlling effect Effects 0.000 description 13
- 238000000465 moulding Methods 0.000 description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 230000001105 regulatory effect Effects 0.000 description 11
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 10
- 238000009826 distribution Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- 238000001179 sorption measurement Methods 0.000 description 9
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 7
- 238000000227 grinding Methods 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 238000011160 research Methods 0.000 description 7
- 230000009286 beneficial effect Effects 0.000 description 6
- 229910010293 ceramic material Inorganic materials 0.000 description 6
- 230000008859 change Effects 0.000 description 6
- 229910052593 corundum Inorganic materials 0.000 description 6
- 239000010431 corundum Substances 0.000 description 6
- 239000004570 mortar (masonry) Substances 0.000 description 6
- 238000007664 blowing Methods 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
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- 238000012360 testing method Methods 0.000 description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 229910052906 cristobalite Inorganic materials 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002073 nanorod Substances 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 229910052681 coesite Inorganic materials 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229910015667 MoO4 Inorganic materials 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229910002808 Si–O–Si Inorganic materials 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
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- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- DERZBLKQOCDDDZ-JLHYYAGUSA-N cinnarizine Chemical compound C1CN(C(C=2C=CC=CC=2)C=2C=CC=CC=2)CCN1C\C=C\C1=CC=CC=C1 DERZBLKQOCDDDZ-JLHYYAGUSA-N 0.000 description 1
- 229960000876 cinnarizine Drugs 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 229910052634 enstatite Inorganic materials 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005496 eutectics Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000007716 flux method Methods 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
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- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000009766 low-temperature sintering Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- BBCCCLINBSELLX-UHFFFAOYSA-N magnesium;dihydroxy(oxo)silane Chemical compound [Mg+2].O[Si](O)=O BBCCCLINBSELLX-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000002082 metal nanoparticle Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000005543 nano-size silicon particle Substances 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229910052604 silicate mineral Inorganic materials 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000009210 therapy by ultrasound Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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Abstract
The invention relates to a mullite whisker-attapulgite porous ceramic with high specific surface area and a preparation method thereof, wherein the preparation method comprises the steps of firstly mixing attapulgite, silicon carbide and aluminum sulfate and carrying out ball milling to obtain ceramic mixed powder; mixing the ceramic powder with Li2MoO4、Na2MoO4Mixing and ball-milling to obtain mixed powder of ceramic powder and molten salt; then, performing cold isostatic pressing and pre-pressing on the mixed powder to form a ceramic blank; and finally, carrying out low-temperature calcination and post-treatment on the ceramic body to obtain the mullite whisker-attapulgite porous ceramic. Compared with the prior art, the invention adopts the molten salt method to assist the in-situ reaction sintering method to prepare the nano-particlesThe mullite whisker-attapulgite porous ceramic with the self-assembly structure of the rod-shaped crystal, uniformly distributed multi-stage pores and larger specific surface area has the advantages of low preparation temperature, simple and controllable process, high reaction sintering efficiency, low requirement on equipment and the like.
Description
Technical Field
The invention belongs to the technical field of materials, and relates to mullite whisker-attapulgite porous ceramic with high specific surface area and a preparation method thereof.
Background
Attapulgite (Attapulgite) is a layer chain-shaped water-containing magnesium-rich aluminum silicate clay mineral with nanorod crystal morphology (about 0.5-5 μm in length and about 20-70nm in diameter) and regular nanopores (0.37nm multiplied by 0.64nm), has low thermal conductivity (0.06W/(m.K)), and large specific surface area (up to 350m & lt/m & gt)2g-1Above), surface charge and cation exchange capacity and low density (2.05-2.32g cm)-3) The method is widely used for preparing adsorbents, adhesives, drying agents, catalysts, food additives and functional composite materials, and plays an irreplaceable important role as a basic material in the fields of chemical industry, catalysis, environmental protection, new materials and the like. The theoretical chemical formula of the attapulgite crystal is Mg5Si8O20(OH)2(OH2)4·4H2And O. However, during the formation process of attapulgite, Mg (II) ions in the crystal structure are often replaced by metal ions such as Al (III), Fe (II) and the like, and the attapulgite has negative charge and cation adsorption capacity as a result of isomorphous replacement and simultaneously has unique propertyThe attapulgite clay has a special rod-shaped microcrystalline structure and a pore passage, and the naturally produced attapulgite clay has better adsorption performance on pollutants such as heavy metals, dyes, antibiotics and the like; the attapulgite is hydrophilic on the surface, so the adsorption capacity to pollutants such as hydrophobic organic matters, non-polar molecules and the like is limited, and the wide application of the attapulgite as an adsorbent is restricted [ Li Yi Jing, Xie Xin, Yuan Miao, Liu Fang, Su Qiong, Wang hong Ling, Panpaofeng, Wang Yan and attapulgite modification method and research progress [ J yan and J attapulgite modification method and research progress ]]Current chemical research 2020,3: 124-.]And [ Peiyi Bao, Haiying Du, Xianning xu, Junya Li, Yao Wu, Shaojiang Zhou, Lingyun Li, Ningfei Lei.Adsoperation of Cr (VI) onto Attapulgite/UiO-66-NH2Composites from Aqueous Solution[J].IntegratedFerroelectrics.2020,209:125–134.]. In addition, the research shows that the attapulgite can generate phase change (converted into enstatite and cristobalite) under the condition that the temperature exceeds 700 ℃, and the fibrous structure is damaged, so that the specific surface area of the attapulgite is greatly reduced [ Yurongtai, Von Jie, Maxiang, Liufang, Wanyawei, Shexingpeng, Wanchangan]Ceramic bulletin, 2016,37(5):531-535.]And [ Liubin, Wangping, cinnarizine, Penghu, Conbang, attapulgite adsorption functional ceramic material preparation and crystal form transformation [ J ] at low temperature]The journal of materials science and engineering, 2016,34(3): 404-.]. Therefore, the attapulgite is functionally modified to different degrees by adopting different methods or treatment modes, and the method is an important way for improving the adsorption property and expanding the application temperature. The method has important significance for development, utilization and reprocessing of attapulgite minerals.
At present, the common attapulgite modification methods mainly comprise a physical method and a chemical method. The physical modification method comprises grinding, ball milling, ultrasonic treatment, high-speed stirring, irradiation treatment, etc., and mainly dissociates attapulgite rod crystal beams under the action of mechanical force, thereby improving the dispersibility and specific surface area of the rod crystal and simultaneously releasing more surface active groups; or breaking the rod crystal to form new silicon hydroxyl on the surface; or the high-energy rays are used for changing the rod crystal aggregation state or activating inert Si-O-Si groups and the like, and the effects are favorable for improving the adsorption performance of the attapulgite. The chemical modification method mainly comprises hydrothermal treatment, acid or alkali treatment, heat treatment, organic modification treatment (such as organic solvent treatment, water-soluble organic solvent treatment, etc.),Organic acid treatment, surface grafting functional group and the like) and nano composite modification (such as loading noble metal nano particles and magnetic metal oxide Fe3O4And polymers thereof [ li yijing, xixin, Yuanyao, salicylic, Suqiong, Wanhongling, Ponkongfeng, Wang and attapulgite ] modification method and research progress [ J-shaped scaffold]Current chemical research 2020,3: 124-.]And [ Junbin Shi, Min Li, Surface modification effects in phase change-encapsulated attribute [ J].Materials Chemistry and Physics,2020,254:123521.]. On the other hand, the porous ceramic block structure has the advantages of large specific surface area, good high-temperature stability and the like, so if the attapulgite can be prepared into the porous ceramic block structure, the specific surface area of the attapulgite can be effectively improved, the surface groups and the charge state can be improved or the ion exchange capacity can be improved while the original fibrous structure is kept, but the related research reports are less.
Disclosure of Invention
The invention aims to provide a high-specific surface area mullite whisker-attapulgite porous ceramic and a preparation method thereof, which are used for solving the problems that the attapulgite has poor dispersibility, undergoes phase change and sintering at high temperature and cannot keep the original rod-like and pore structure. On one hand, the dispersion and the specific surface area of the attapulgite are greatly improved through a porous composite structure assembled by mullite whiskers and nano rods, so that the adsorption performance of the attapulgite is improved, and the application range of the attapulgite is expanded; on the other hand, the combination of the molten salt method and the in-situ reaction sintering method can realize the composition of the mullite in-situ and the attapulgite at low temperature, thus being beneficial to the low-temperature sintering molding of the attapulgite, keeping the original nano rod-shaped structure and simultaneously improving the service temperature (above 700 ℃) of the attapulgite-based ceramic.
The purpose of the invention can be realized by the following technical scheme:
a preparation method of mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, silicon carbide and aluminum sulfate and ball-milling to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Mixing and ball-milling to obtain mixed powder of ceramic powder and molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank;
4) and (3) sequentially carrying out low-temperature calcination and post-treatment processes on the ceramic body to obtain the mullite whisker-attapulgite porous ceramic.
Further, in the step 1), the molar ratio of the attapulgite, the silicon carbide and the aluminum sulfate is (2-20) to (1-6) to (1-12).
The nanometer silicon carbide has two functions: on the one hand, silicon carbide as a silicon source is subjected to oxidation reaction with oxygen and sulfur trioxide (aluminum sulfate is decomposed at high temperature to generate sulfur trioxide and aluminum oxide) in molten salt to generate SiO2Further generating mullite with alumina (the aluminum sulfate is decomposed at high temperature to generate sulfur trioxide and alumina); on the other hand, oxidation of silicon carbide produces CO2Or CO gas escapes, so that pores exist in the ceramic to be used as pore-forming agents.
Aluminum sulfate also has two effects: in one aspect, aluminum sulfate acts as an aluminum source and decomposes at high temperatures to produce sulfur trioxide and alumina, which reacts with the resulting SiO in a molten salt2Carrying out in-situ reaction with the quartz phase in the attapulgite raw material to generate mullite; on the other hand, sulfur trioxide generated by decomposing aluminum sulfate can be used as an oxidant to further oxidize SiC to generate SiO2With simultaneous generation of gas (CO)2Or CO) to prepare a porous ceramic.
Mullite (3 Al)2O3·2SiO2Mullite) is a ceramic that readily forms acicular crystals, and has good high temperature stability, oxidation resistance, low oxygen permeability, low thermal conductivity, and a high melting point (1900 ℃). The invention introduces mullite whiskers into the attapulgite by combining a molten salt method and an in-situ reaction sintering method to prepare the whisker and nanorod assembled composite porous ceramic.
As a preferable technical proposal, the length of the attapulgite is 100-200nm, and the diameter is 20-40 nm.
As a preferable technical scheme, the silicon carbide comprises nanometer silicon carbide powder with the grain diameter of 40-60nm, and the grain diameter is more preferably 50 nm.
A large number of experiments prove that the limitation of the particle size range of the silicon carbide is beneficial to: (1) the 40-60nm nanometer silicon carbide powder has higher reaction activity and is easy to be oxidized to generate nanometer SiO2Thereby being beneficial to generating mullite whiskers in the molten salt environment finally; (2) the nano silicon carbide in the particle size range is used as a pore-forming agent, so that the porous ceramic with a micro-nano pore structure required by the application can be formed, and the specific surface of the finally obtained porous ceramic is also optimal.
Further, in the step 1), the ball milling equipment is a planetary ball mill, the ball milling medium is isopropanol, and the ball milling time is 8-48 h.
Further, in the step 2), the ceramic mixed powder and Li2MoO4、Na2MoO4The mass ratio of (1-10) to (1-5).
Wherein Li2MoO4、Na2MoO4As a molten salt system for use in the molten salt process of the present invention.
The molten salt method, also called flux method, is to dissolve the raw materials in the molten salt melt at high temperature to form a saturated solution, and then to precipitate crystals from the solute in the saturated solution by slow cooling or flux evaporation to obtain the chemical substance to be prepared. The molten salt system is selected according to the following: (1) the melting temperature of the molten salt can be adapted to the temperature of the synthesized substance, and the chemical composition change of the synthesized substance cannot be caused by adding the molten salt; (2) the molten salt is selected to have a greater solubility (in water); the fused salt can be removed by washing out after the powder is synthesized, and a high-purity product is obtained. The fused salt method for synthesizing powder has two reaction mechanisms: (1) based on the medium diffusion principle, the reaction mechanism is that chemical raw materials are firstly dissolved in molten salt, the raw materials of all components carry out chemical reaction, and when the product of the chemical reaction is saturated, precipitation is generated to form crystal precipitation; (2) based on the theory of dissolution speed difference, in the same molten salt, because the dissolution speeds of reactants in the molten salt are different, reaction components with high dissolution speed are quickly diffused to the surface of a substance with low dissolution speed, and the reaction components and the substance react with each other to form a product. The synthesis of materials by the molten salt method generally involves two processes of nucleation and growth of crystals, which are divided into three stages: firstly, contacting and mixing molten salt and chemical raw materials; secondly, fusion, chemical reaction recombination and diffusion between the molten salt and the reaction raw materials; third, crystal growth and washing out. The invention provides a low-temperature molten salt method for preparing mullite whisker-attapulgite porous ceramic, which solves the problems of high-temperature phase change of attapulgite material and difficult retention of rod-shaped porous channel structure on the one hand; on the other hand, the composition of the mullite whiskers and the attapulgite in the attapulgite is realized by an in-situ reaction sintering method, the uniform dispersion of a rod-shaped structure in the attapulgite is promoted, and the specific surface area of the porous ceramic is improved. The method has the advantages that the mullite whiskers and the attapulgite are uniformly dispersed, and the whiskers and the rod-shaped structures are self-assembled into micro-nano structures under the condition of a molten salt method, so that micro-nano holes with different sizes are formed, meanwhile, the pores are formed by gas generated in the reaction sintering process, micropores with larger sizes are formed, and further, porous ceramics with larger specific surface and multistage pore distribution are formed.
At present, LiCl (melting point: 605 ℃ C.), KCl (melting point: 770 ℃ C.), NaCl (melting point: 801 ℃ C.), and Na are commonly used as molten salts2SO4(melting point 884 ℃ C.), Na2MoO4(680 ℃ C.) and Li2MoO4(705 ℃ C.), etc.
In the present application, Li is selected2MoO4And Na2MoO4The fused salt system is proved by a large number of experiments, and the specific reasons are as follows: (1) in order to prepare the porous ceramic at low temperature and retain the structure and the composition of the attapulgite, the mullite-attapulgite porous ceramic prepared by the method needs to select a low-temperature molten salt system, and Na2MoO4(melting point 680 ℃ C.) and Li2MoO4(the melting point is 705 ℃) compared with other molten salts, the melting points are below 700 ℃, and the eutectic temperature of the molten salts and the viscosity of the molten salts are further regulated and controlled by controlling the proportion of the two molten salts; (2) SiO produced by oxidation in the above molten salt2Has proper solubility with alumina, and is favorable to diffusion-mass transferSo as to generate chemical reaction; (3) by regulating the proportion of molybdate molten salt and the sintering temperature, the viscosity and the fluidity of the molten salt can be further regulated, so that the nucleation-growth rate of mullite is regulated, and the mullite is favorably oriented to grow into whiskers; (4) the low-temperature viscosity and the low-temperature fluidity of the molybdate further influence the escape of gas in a reaction system, thereby being beneficial to regulating and controlling the pore structure of the porous ceramic.
Further, in the step 2), the ball milling equipment is a planetary ball mill, the ball milling method is dry ball milling, and the ball milling time is 2-8 h.
Further, in the step 3), in the cold isostatic pressing forming process, the forming pressure is 30-90MPa, and the forming time is 3-15 min.
The purpose of cold isostatic pressing and pre-pressing forming and the reason for limiting the forming pressure are as follows: through a large number of experiments: (1) the purpose of cold isostatic pressing is to obtain a later-stage porous ceramic block, and the cold isostatic pressing can ensure that the ceramic blank is uniformly pressed in all directions and ensure that the later-stage porous ceramic has uniform and isotropic structure in all directions; (2) the pressure limit of the cold isostatic pressing is a range obtained through a large number of experiments, and the pressure limit is used for ensuring that the block ceramic is fully contacted with molten salt and among reaction raw materials in-situ reaction sintering in a molten salt environment, and the pore structure of the porous ceramic prepared in the later stage can be regulated and controlled, so that the mullite whisker-attapulgite porous ceramic with the controllable specific surface area is prepared.
Further, in the step 4), in the low-temperature calcination process, the calcination temperature is 500-900 ℃, and the calcination time is 1-8 h.
The calcination temperature is a range obtained by a number of experiments and is limited for the following reasons: (1) by controlling the proper calcination temperature and further controlling the viscosity and the fluidity of the molten salt system, the method can be beneficial to the full diffusion and contact of reactants to fully generate a chemical reaction to generate mullite; (2) the proper calcination temperature can control the form and microstructure of the concave-convex rod in the mullite whisker-attapulgite porous ceramic, so as to obtain porous ceramics with different compositions and structures, and the sintering temperature directly influences the porosity of the porous ceramic (on the premise of controlling other parameters to be unchanged, the sintering temperature is high, the porosity is reduced, the sintering temperature is reduced, and the porosity is increased); (3) by regulating and controlling the sintering temperature, the nucleation-growth rate of the mullite in the molten salt is further regulated and controlled, and the mullite oriented growth is favorably regulated and controlled to form whiskers; (4) the sintering temperature directly influences the viscosity and the fluidity of a molybdate molten salt system and further influences the escape rate of gas in a reaction system, thereby being beneficial to regulating and controlling the pore structure of the porous ceramic.
Furthermore, in the low-temperature calcination process, the heating rate and the cooling rate are both 3-8 ℃/min.
As a preferred technical scheme, the heating rate and the cooling rate are both 5 ℃/min.
Further, in the step 4), the post-treatment process sequentially comprises a boiling water dipping process and an electric heating forced air drying process; wherein,
in the boiling water dipping process, the dipping temperature is 60-100 ℃, and the dipping time is 1-8 h;
in the electric heating forced air drying process, the drying temperature is 80-120 ℃, and the drying time is 4-12 h.
The mullite whisker-attapulgite porous ceramic with high specific surface area is prepared by the method, the porosity of the obtained mullite whisker-attapulgite porous ceramic is 15-90%, and the specific surface area is 10-60m2g-1。
On one hand, the mullite whisker-attapulgite porous ceramic with gradient pore size distribution is prepared in one step by adopting a molten salt method assisted in-situ reaction sintering method, and a whisker-nanorod self-assembled micro-nano structure can be effectively formed, so that the dispersity of an attapulgite rod-shaped structure is improved, the specific surface area of the porous ceramic is increased, and the adsorption performance and the high-temperature stability of the porous ceramic are optimized and improved; on the other hand, the sintering and forming temperature of the mullite whisker and the attapulgite is greatly reduced by reaction and sintering in a molten salt environment, and the phase change of the attapulgite at high temperature and the damage of the original rod-shaped and pore channel structures are inhibited. Therefore, the invention provides the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area, which has low preparation cost, simple operation and controllable porous structure and has wide development prospect.
In the mullite whisker-attapulgite porous ceramic, the attapulgite belongs to silicate minerals according to the chemical composition and structure of the attapulgite, and both the attapulgite and the mullite whisker belong to silicate ceramics, and the chemical compatibility of the attapulgite and the mullite whisker is better. Thus, both are present in the product in the form: (1) the mullite forms a porous ceramic whisker framework in the product, and the acicular or rod-shaped attapulgite with the nanometer pore channels is dispersed and distributed in the mullite whisker framework, so that the specific surface area of the porous ceramic is synergistically improved, and can be proved by a mullite whisker-attapulgite porous ceramic SEM photograph shown in figure 2; (2) the original quartz phase of the attapulgite is used as a silicon source and also participates in-situ reaction sintering to generate mullite whiskers, so that the mullite and the attapulgite are promoted to be directly bonded by strong chemical bonds, namely, the bonding form of the mullite and the attapulgite has both whisker-rod-shaped woven bonding formed physically and chemical bonding.
Compared with the prior art, the invention has the following characteristics:
1) the invention takes the attapulgite as the ceramic matrix, and adopts a low-temperature molten salt method to assist the in-situ reaction sintering to prepare the mullite whisker-attapulgite porous ceramic, and the porous ceramic has the advantages of uniform pore size distribution, high specific surface area, better adsorption performance and the like;
2) the homogeneous compounding of mullite whiskers and attapulgite is further realized by a low-temperature molten salt method assisted in-situ reaction sintering method, the micro-nano porous ceramic with multi-level pores is formed, the problems of high-temperature phase change of the attapulgite material and difficulty in retaining a rod-shaped porous channel structure are solved, the homogeneous dispersion of the rod-shaped structure in the attapulgite is promoted, and the specific surface area of the composite porous ceramic is further improved;
3) the preparation method of the mullite whisker-attapulgite porous ceramic has the advantages of low preparation temperature, simple and controllable process, high reaction sintering efficiency, low requirement on equipment and the like;
4) the porosity and the specific surface area of the mullite whisker-attapulgite porous ceramic can be flexibly regulated and controlled and are respectively 15-90 percent and 10-60m2g-1。
Drawings
FIG. 1 is an XRD pattern of the mullite whisker-attapulgite porous ceramic prepared in example 2;
fig. 2 is an SEM photograph of the mullite whisker-attapulgite porous ceramic prepared in example 2.
Detailed Description
The invention is described in detail below with reference to the figures and specific embodiments.
The preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of (2-20) to (1-6) to (1-12), placing the mixture in a planetary ball mill, ball-milling for 8-48h by taking isopropanol as a ball-milling medium, drying, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to the mass ratio of (1-10) to (1-5), placing the mixture in a planetary ball mill, and carrying out dry ball milling and mixing for 2-8h to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 30-90MPa, and the molding time is 3-15 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 1-8h in a high-temperature box furnace at the temperature of 500-900 ℃, and controlling the heating rate and the cooling rate to be 3-8 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distributions and containing molten salt;
5) the mullite whisker-attapulgite porous ceramic containing the fused salt is immersed in a water bath environment, heated to 60-100 ℃ and boiled for 1-8h to remove the soluble fused salt in the porous ceramic, and then the mullite whisker-attapulgite porous ceramic is taken out and put into an electric heating forced air drying oven at 80-120 ℃ to be dried for 4-12h, so that the mullite whisker-attapulgite porous ceramic with uniformly distributed pores is obtained.
The attapulgite in the following examples is purchased from Feizhou New Material Co., Ming Guang, Anhui province, the length of the attapulgite is 100-200nm, and the diameter is 20-40 nm; what is needed isThe ball mill is a QM-3SP4 type planetary ball mill produced by Nanjing university; the silicon carbide is nano silicon carbide powder which is purchased from Anhui Hefei Kerr nano energy science and technology Limited and has the grain diameter of 40-60nm (preferably 50 nm); isopropanol and Al2(SO4)3·18H2O、Li2MoO4And Na2MoO4All are analytical pure reagents with the purity of more than or equal to 99.7 percent; the cold isostatic pressing equipment is a YLJ-CIP-20B manual split type cold isostatic pressing machine produced by Anhui Hefei crystal material technology Limited; the constant temperature water bath kettle is a ZKYY-2L type intelligent water bath kettle produced by Instrument GmbH of Jiangsu province and Jiangyi city; the used electric heating air blast drying oven is a DHG-9075A type electric heating air blast drying oven produced by Shanghai-Hengyue scientific instruments Co., Ltd; the high-temperature box furnace is a Naberterm GmbH 1300 ℃ high-temperature furnace.
The present embodiment is implemented on the premise of the technical solution of the present invention, and a detailed implementation manner and a specific operation process are given, but the scope of the present invention is not limited to the following embodiments.
Example 1:
the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of 2:2:3, placing the mixture in a planetary ball mill, ball-milling for 8 hours by using isopropanol as a ball-milling medium, drying, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to a mass ratio of 4:3:2, placing the mixture in a planetary ball mill, and performing dry ball milling and mixing for 4 hours to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 40MPa, and the molding time is 10 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 6 hours in a high-temperature box furnace at 600 ℃, and controlling the heating rate and the cooling rate to be 5 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distribution and containing molten salt;
5) immersing the mullite whisker-attapulgite porous ceramic containing the molten salt in a water bath environment, heating to 80 ℃, boiling for 7h to remove the soluble molten salt in the porous ceramic, taking out, and then drying in an electrothermal blowing dry box at 80 ℃ for 12h to obtain the mullite whisker-attapulgite porous ceramic with uniformly distributed pores, wherein the porosity of the porous ceramic material is 80 percent and the specific surface area is 50m through tests2g-1。
Example 2:
the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of 5:1:2, placing the mixture in a planetary ball mill, ball-milling the mixture for 12 hours by using isopropanol as a ball-milling medium, drying the mixture, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to the mass ratio of 2:1:1, placing the mixture in a planetary ball mill, and performing dry ball milling and mixing for 6 hours to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 60MPa, and the molding time is 8 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 4 hours in a high-temperature box furnace at 800 ℃, and controlling the heating rate and the cooling rate to be 5 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distribution and containing molten salt;
5) immersing the mullite whisker-attapulgite porous ceramic containing the molten salt in a water bath environment, heating to 90 ℃, boiling for 4h to remove the soluble molten salt in the porous ceramic, taking out, then placing in an electrothermal blowing drying oven at 90 ℃ for drying for 8h to obtain the mullite whisker-attapulgite porous ceramic with uniformly distributed pores, testing,the porosity of the porous ceramic material is 60 percent, and the specific surface area is 40m2g-1。
Fig. 1 shows the XRD pattern of the mullite whisker-attapulgite porous ceramic prepared in this example. As can be seen from the figure: the mullite whisker-attapulgite porous ceramic has good crystallinity, mainly consists of two crystal phases of mullite and attapulgite, and standard cards corresponding to the crystal phases are PDF NO.15-0776 and PDF NO.31-0783 respectively.
Fig. 2 shows an SEM photograph of the mullite whisker-attapulgite porous ceramic prepared in this example. As can be seen from the figure: the mullite whisker-attapulgite porous ceramic has a porous structure, the micron and nanometer pores are uniformly distributed, and the maximum diameter of the micropore is about 23 mu m; the mullite is woven together in a whisker shape, and the attapulgite is uniformly dispersed and distributed in the mullite whisker and still keeps the rod-shaped crystal structure.
Example 3:
the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of 10:3:6, placing the mixture in a planetary ball mill, ball-milling the mixture for 36 hours by using isopropanol as a ball-milling medium, drying the mixture, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to the mass ratio of 10:4:1, placing the mixture in a planetary ball mill, and performing dry ball milling and mixing for 8 hours to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 80MPa, and the molding time is 5 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 2h in a high-temperature box furnace at 900 ℃, and controlling the heating rate and the cooling rate to be 5 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distribution and containing molten salt;
5) immersing the mullite whisker-attapulgite porous ceramic containing the molten salt in a water bath environment, heating to 100 ℃, boiling for 2h to remove the soluble molten salt in the porous ceramic, taking out, and then drying in an electrothermal blowing dry box at 120 ℃ for 4h to obtain the mullite whisker-attapulgite porous ceramic with uniformly distributed pores, wherein the porosity of the porous ceramic material is 30 percent and the specific surface area is 20m through tests2g-1。
Example 4:
the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of 2:1:1, placing the mixture in a planetary ball mill, ball-milling for 9 hours by using isopropanol as a ball-milling medium, drying, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to the mass ratio of 1:1:1, placing the mixture in a planetary ball mill, and performing dry ball milling and mixing for 2 hours to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 30MPa, and the molding time is 15 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 8 hours in a high-temperature box furnace at 500 ℃, and controlling the heating rate and the cooling rate to be 8 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distribution and containing molten salt;
5) immersing the mullite whisker-attapulgite porous ceramic containing the molten salt in a water bath environment, heating to 60 ℃, boiling for 8h to remove the soluble molten salt in the porous ceramic, taking out, and then drying in an electrothermal blowing dry box at 90 ℃ for 10h to obtain the mullite whisker-attapulgite porous ceramic with uniformly distributed pores, wherein the porosity of the porous ceramic material is 15 percent and the specific surface area is 10m through tests2g-1。
Example 5:
the preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area comprises the following steps:
1) mixing attapulgite, nano silicon carbide powder and Al2(SO4)3·18H2Mixing O uniformly according to a molar ratio of 10:3:6, placing the mixture in a planetary ball mill, ball-milling for 48 hours by using isopropanol as a ball-milling medium, drying, and grinding the mixture by using an agate mortar for later use to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Uniformly mixing the ceramic powder and the molten salt according to the mass ratio of 2:1:1, placing the mixture in a planetary ball mill, and performing dry ball milling and mixing for 8 hours to obtain uniform mixed powder of the ceramic powder and the molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank; wherein the molding pressure is 90MPa, and the molding time is 3 min;
4) placing the ceramic blank in a corundum crucible, sintering and preserving heat for 1h in a high-temperature box furnace at 900 ℃, and controlling the heating rate and the cooling rate to be 3 ℃/min to obtain mullite whisker-attapulgite porous ceramic with different pore-size structures and distribution and containing molten salt;
5) immersing the mullite whisker-attapulgite porous ceramic containing the molten salt in a water bath environment, heating to 100 ℃, boiling for 1h to remove the soluble molten salt in the porous ceramic, taking out, and then drying in an electrothermal blowing dry box at 120 ℃ for 4h to obtain the mullite whisker-attapulgite porous ceramic with uniformly distributed pores, wherein the porosity of the porous ceramic material is 90 percent and the specific surface area is 60m through tests2g-1。
The embodiments described above are described to facilitate an understanding and use of the invention by those skilled in the art. It will be readily apparent to those skilled in the art that various modifications to these embodiments may be made, and the generic principles described herein may be applied to other embodiments without the use of the inventive faculty. Therefore, the present invention is not limited to the above embodiments, and those skilled in the art should make improvements and modifications within the scope of the present invention based on the disclosure of the present invention.
Claims (10)
1. A preparation method of mullite whisker-attapulgite porous ceramic with high specific surface area is characterized by comprising the following steps:
1) mixing attapulgite, silicon carbide and aluminum sulfate and ball-milling to obtain ceramic mixed powder;
2) mixing ceramic powder with Li2MoO4、Na2MoO4Mixing and ball-milling to obtain mixed powder of ceramic powder and molten salt;
3) carrying out cold isostatic pressing on the mixed powder for forming to obtain a ceramic blank;
4) and (3) sequentially carrying out low-temperature calcination and post-treatment processes on the ceramic body to obtain the mullite whisker-attapulgite porous ceramic.
2. The method for preparing the mullite whisker-attapulgite porous ceramic with high specific surface area as claimed in claim 1, wherein the molar ratio of the attapulgite, the silicon carbide and the aluminum sulfate in the step 1) is (2-20) to (1-6) to (1-12).
3. The preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area according to claim 1, wherein in the step 1), the ball milling equipment is a planetary ball mill, the ball milling medium is isopropanol, and the ball milling time is 8-48 h.
4. The method for preparing the mullite whisker-attapulgite porous ceramic with high specific surface area according to claim 1, wherein in the step 2), the ceramic mixed powder is mixed with Li2MoO4、Na2MoO4The mass ratio of (1-10) to (1-5).
5. The preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area as claimed in claim 1, wherein in the step 2), the ball milling equipment is a planetary ball mill, the ball milling method is dry ball milling, and the ball milling time is 2-8 h.
6. The preparation method of the mullite whisker-attapulgite porous ceramic with high specific surface area as claimed in claim 1, wherein in the step 3), the forming pressure is 30-90MPa and the forming time is 3-15min during the cold isostatic pressing forming process.
7. The method for preparing the mullite whisker-attapulgite porous ceramic with high specific surface area as claimed in claim 1, wherein in the step 4), the calcination temperature is 500-900 ℃ and the calcination time is 1-8h in the low-temperature calcination process.
8. The method for preparing the mullite whisker-attapulgite porous ceramic with high specific surface area according to claim 7, wherein the heating rate and the cooling rate are both 3-8 ℃/min in the low-temperature calcination process.
9. The method for preparing the mullite whisker-attapulgite porous ceramic with high specific surface area according to claim 1, wherein in the step 4), the post-treatment process sequentially comprises a boiling water impregnation process and an electric heating forced air drying process; wherein,
in the boiling water dipping process, the dipping temperature is 60-100 ℃, and the dipping time is 1-8 h;
in the electric heating forced air drying process, the drying temperature is 80-120 ℃, and the drying time is 4-12 h.
10. The mullite whisker-attapulgite porous ceramic with high specific surface area is characterized by being prepared by the method as claimed in any one of claims 1 to 9.
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